Dehumidification method and plant particularly for granular materials

ABSTRACT

The present invention relates to a granular-material dehumidification plant including at least one silo or hopper ( 1 ) arranged to receive granular material ( 2 ) to be dehumidified at the top thereof and provided with a controlled lower delivering mouth ( 3 ), at least one feeding duct ( 8, 10 ) designed to be dipped in the granular material ( 2 ) contained in each hopper ( 1 ) to supply hot and dry processing air thereto, and at least one exhaust duct ( 5 ) for humid processing air; at least two molecular sieve towers ( 68, 69 ) arranged alternately to supply hot and dry processing air to the at least one hopper, each tower delimiting therein a space ( 67 ) for housing molecular sieves and a chamber ( 70 ) for housing heating means, the space and the chamber being in fluid communication with one another at one end thereof, while being in fluid communication, at the other end thereof, with a respective air inlet/outlet duct ( 65, 73; 66, 74 ); air pressurizing or pumping means ( 13 ) arranged to receive, at the suction (inlet) side thereof, humid processing air from a respective exhaust duct ( 5 ), and to feed pressured air, at the delivery side thereof, to each molecular sieve tower ( 68, 69 ); switching-shunting means ( 24 ) located between the delivery of the pressurizing means and the inlet/outlet ducts of the housing spaces ( 67 ) for molecular sieves thereby switching at least one of the molecular sieve towers between a processing step and a regeneration step; and a programmable electronic control unit ( 15 ). The granular-material dehumidification plant further comprises pressurizing valve means ( 77 ) located between the inlet/outlet ducts ( 73, 74 ) of the housing chamber ( 70 ) of the heating means for each molecular sieve tower ( 68, 69 ) and arranged to ensure a minimum pressure within a tower during a regeneration step, and temperature detecting means electrically connected to an input of the programmable electronic control unit.

The present invention relates to a flexible operation dehumidification plant and method for granular materials, particularly suitable for granular materials comprising one or more plastic materials.

In the description of the present invention, the term “granular” refers both to proper granules and pieces of ground or triturated plastic material, which can include scale pieces, pieces of laminar material, i.e. also pieces with a predominant plane surface.

In the methods for transforming plastic materials, the dehumidification processing is very important, particularly before a melting step at high temperature of the granular material. During the dehumidification treatment, water contained, or otherwise connected to granules of the granular material, in particular of those so called “hygroscopic” granular materials, is removed. The humidity removing from the granular material is necessary because, during softening and hot melting, water would insinuate itself into the polymers molecular chains then breaking them, which would translate in bubbles, blowholes, and both structural and colouring unhomogeneity to be formed during cooling, thereby obtaining a final transformed plastic material presenting poor mechanical characteristics.

Dehumidification plants for granular materials, said dehumidifiers or dryers, have just been proposed and, among these, that providing use of the so called molecular sieves are imposed, which molecular sieves have the property, at room temperature, of absorbing the humidity of the water passing therethrough in a almost complete way. The molecular sieves are contained in a suitable container, also said tower, provided with a humid air inlet, on one hand, and with dry air outlet on the other. The air made dry by the molecular sieves is heated and then passes through the bulk of granular material to be dehumidified, which thus gradually transfers the humidity contained therein to the dry and hot air. The duration of the dehumidification process depends on different factors, such as humidity residual content, temperature and flow of dry air. The absorption capacity of the molecular sieves is nevertheless quantitatively limited and after a certain time saturation is reached. For this reason, a sieve assembly is used provided in suitable containers which can be connected in parallel, whereby after saturation of the molecular sieves in a container, humid air is supplied to another sieve container, whereas the saturated one is subjected to a regeneration treatment. Then, most of dehumidification plants often operate with two containers of molecular sieves, which work according to an alternating cycle. A new dehumidification plant according to the prior art is taught in EP-1 475 593 to the applicant of the present invention.

Till now known dehumidification plants, although satisfactory from many points of view, are of a “rigid” type, i.e. they do not permit the dry air flow-rate to be varied in accordance with the actual use requirements, whereby treatment steps can occur in which there is an excess of dry heating air supplying with consequent waste of energy.

The main object of the present invention is to provide a flexible dehumidification method, in the sense of permitting to vary the dry air flow-rate coming out from each tower or container of molecular sieves as a function of a predetermined number of operating parameters of the plant.

Another object of the present invention is that said dehumidification method makes it possible to carry out a right regeneration of each containers of molecular sieves in independent from possible flow-rate variations in the process air flow.

Another object of the present invention is that said dehumidification method permits a substantial saving of heat energy to be obtained.

A further object of the present invention is that to provide a dehumidification plant which is capable to carry out in an optimum way the variable flow-rate dehumidification process of the present invention.

According to a first aspect of the present invention, there is provided a dehumidification plant for granular materials including at least one silo or hopper for containing and dehumidifying granular material, which is provided with a controlled lower supplying mouth, at least one feeding duct for hot and dry process air designed to draw within the granular material contained in each hopper, and at least one exhaust duct for humid process air; at least two molecular sieve towers arranged to alternately supply hot and dry process air to each hopper, each delimiting a housing chamber for molecular sieves and a housing chamber for heating means, said housing chambers being in communication one with another at an end thereof, whereas they are in communication, at their other end, with a respective air inlet/outlet duct; pressurizing or pumping means arranged to receive, at the suction (inlet) side, humid process air from said at least one exhaust duct, and to feed at the delivery side, pressured air to each molecular sieve tower; switching-shunting means placed between the delivery side of said pressurizing means and said inlet/outlet ducts of said housing chambers for molecular sieves in order to switch at least one of said molecular sieve towers between a process step and a regeneration step; and a programmable electronic control unit, characterized in that it comprises pressurizing valve means placed between said inlet/outlet ducts of said housing chamber of said heating means for each molecular sieve tower and arranged to assure a minimum pressure within a tower during the regeneration step, and detecting means for temperature electrically connected to said programmable electronic control unit, at its input.

According to another aspect of the present invention, there is provided a method for regenerating a molecular sieve tower in a dehumidification plant for granular material comprising, in sequence, heating molecular sieves to a temperature of about 300° C., and cooling molecular sieves, characterized in that said cooling comprises a controlled mixing of air within the tower to be cooled with process air coming from another molecular sieve tower, said mixing being controlled through said switching/shunting means in response to the temperature detected by said temperature detecting means.

Further features and advantages of the present invention will better appear from the following detailed description given by way of non-limiting example of carrying out the invention, in union with the accompanying drawings, in which:

FIG. 1 illustrates a diagrammatical view of a variable flow-rate dehumidification plant having two towers according to the present invention with components showed in section for clarity;

FIG. 2 shows in enlarged scale a detail of FIG. 1 concerning a diaphragm valve, but in a different operation trim;

FIG. 3 is a cross-sectional view in enlarged scale of a slide valve shown in FIG. 1;

FIG. 4 is a perspective view with cut-out portions of a driving assembly of the slide valve of FIG. 3; and

FIG. 5 illustrates a cross-sectional view and in enlarged scale of a pressurizing valve shown in FIG. 1.

With reference to the above mentioned Figures, it will be noted as a dehumidification plant according to the present invention is formed by one or more silos or hoppers 1 designed to contain a bulk of granular material 2 to be dehumidify. Each hopper 1 has a bottom provided with wall or wall that are tilted forward a lower exhaust mouth 3 for granular material 2, with the lower exhaust mouth 3 being suitably intercepted by a batching device or extractor (not shown) of any suitable type, as it is usually in the art. Each silos or hopper 1 is closed at its top and presents an outlet mouth 4, which directly communicates with an end of an air exhaust duct 5, in which is preferably inserted a temperature probe 6. Each hopper or silo 1 also has a dry air inlet mouth 7, which preferably is formed in its side wall above the level of the granular material 2 contained therein, and is externally in direct communication with a dry air feeding duct 8, in which a heat probe 9 is provided, whereas it is internally in direct communication, e.g. with a length of a crank pipe 10, drawing into the granular material 2 and ending at the lower portion, i.e. close to and above the exhaust opening 3, with a diffuser 11 having a plurality of outlet holes for air formed in a hollow partially spheric body, so to address a multiplicity of jets to more directions at the lower area of the granular material to be dehumidified present within the hopper. During the plant operation, the or each hopper or silo 1 is continuously loaded from the top with cold granular material 2 through a loading device designed in general with the reference 12 and of any suitable type.

Preferably, measuring means of the air flow-rate entering into the hopper 1 are provided in the hot and dry air feeding duct 8, e.g. a Venture tube 92 provided with a respective differential pressure sensor (not shown and of any suitable type, e.g. as illustrated and described in the patent application VR2005A000128 to the applicant of the present application), electrically connected to the control unit 15.

The dehumidification plant further includes air pressurizing or pumping means, e.g. comprising one or more blowers 13 driven by a respective electric motor 14, and a programmable electronic control unit 15, including a microprocessor, as it is usual in the art and designed to drive each blower 13, as well as other components of the plant, as described below. The suction mouth 16 of each blower communicates with an air inlet duct 17, connected to the outlet of cooling means 18 comprising a beam or group of parallel tubes subject to the action of a fan 19 operable by a respective electric motor 20. The cooling battery 18, receives in turn, at the inlet, air coming from the air exhaust duct 5, preferably after being passed through a filtering assembly 21 of any suitable type. The delivery side 22 of each blower 13 communicates with a delivery duct 23 designed to supply pressurized air to switching-shunting valve means, e.g. a slide shunting or distribution valve assembly 24 of any suitable type. In the inlet air duct 17 a depression intake 25 is provided, which communicates through a duct 26 with a differential pressure detecting means, e.g. a solenoid valve 27 electrically connected to the board 15 and whose operation will be explained below. The latter also communicates, by means of a duct 28, with a pressure intake 29 provided in the delivery duct 23.

The valve assembly 24 is provided with a valve body having an inlet 30, two main inlets/outlets 31, 32, and two secondary outlets 33 and 34, the first secondary outlet 33 being at the side of the inlet/outlet 31, whereas the other outlet 34 is at the side of the inlet/outlet 32. The two secondary outlets 33 and 34 communicate, through a respective duct 35 and 36, with a common manifold 37, which communicates with the inlet 38 of drivable intercepting means, preferably comprising a diaphragm valve 39 delimiting an inner chamber divided in two compartments 40 and 41 by a diaphragm 42, which preferably responds to lower working pressure and resists to temperatures of the order of 220-260° C. or more.

As better illustrated in FIG. 2, the body of diaphragm valve 39 is preferably formed by two half bearings 40 a and 41 a fixed together by means of a plurality of peripheral bolts 41 b, with the diaphragm 42 being interposed therebetween, which also assures the airtight between compartments 40 and 41. The compartment or chamber 40 communicates with the atmosphere or a external recovery system for hot air through openings 43 arranged in the half bearing 40 a, whereas the compartment 41 communicates with the output of the solenoid valve 27 by means of a hole 41 c and a duct 44.

With this construction, if compartment 41 is pressurized through the solenoid valve 27, by supplying pressurized air through the duct 44, the diaphragm 42 bends towards the half bearing 40 a and closes the air inlet 38 (FIG. 2). On the contrary, is the compartment 41 is depressurised by the solenoid valve 27, the diaphragm moves away from the air inlet 38 and air can enter into the valve 39 and flow towards the external ambient through the openings 43. The pressure/depression needed for driving the diaphragm 42 is preferably very low, e.g. in the order of 20-30 mbar, and is supplied by blower 13 by means of the pressure intake 28 and duct 28, or the depression intake 25 and duct 26.

As better illustrated in FIGS. 3 and 4, the slide valve assembly 24 delimits three inner chambers: two side chambers 45 and 46, and an intermediate chamber 47, due to the presence of two partitions 48 and 49, preferably two plane and parallel partitions, each having a through opening 50 and 51 respectively. The openings 50 and 51 are aligned one to another. The side chambers 45 and 46 also have a respective opening 50 a and 51 a formed on the body of the valve assembly 24 for the communication with a respective duct 35 and 36, whereas the intermediate chamber 47 communicates with duct 23. The openings 50, 50 a and 51, 51 a are loosely crossed by a rigid rod 52, which comes out from the valve body of the valve assembly 24, thereby presenting an end thereof coming out from the valve body, in order to connect to control means comprising a linear driving device, e.g. comprising a gear motor, which includes a reversible electric motor 53, and a reduction gear 54 of any suitable type, and a rack 55 formed at the end of the rigid rod 52 coming out from the valve body and cinematically connected to the gear motor by means of a further gear reduction assembly, in the example of FIG. 4 two toothed wheels 89, 90.

The rigid rod supports a pair of shutters: one shutter 56 within the chamber 45 arranged to open and close opening 50 on the partition 48, on one hand, and opening 50 a, on the other, and the other shutter 57 arranged to open and close opening 51 on the partition 49, on one hand, and opening 51 a on the other. The arrangement of the shutters on the rigid rod 52 is such that, when the shutter 56 closes the opening 50 and leaves the opening 50 a open, the shutter 57 leaves the opening 51 open and closes the opening 51 a, whereby the slide valve assembly 24 has two end portions and more intermediate portions, as will be further described below.

To this end, opposite with respect to the rack 55, the rod 52 has two stops 58 and 59 fixed thereto, an end of respective

The two main inlets/outlets 31, 32 communicate with a respective duct 65, 66 in communication with a peripheral annular chamber for housing the molecular sieves 67 of a respective dehumidifying tower 68, 69 of the type described in the above mentioned previous patent EP-1 475 593 of the applicant. Within the annular chamber containing the molecular sieves 67 is delimited an inner chamber for housing heating means or hear source (typically one or more electrical resistors 70) designed to transmit heat to the air passing through the inner chamber. The annular chamber and the inner chamber communicate one with another at an end thereof (below), whereas at their other end, they communicate with a respective air inlet/outlet duct, as described below.

At the top of each dehumidifying tower 68, 69 there is provided an air inlet/outlet, respectively 71, 72, which, at the inner of the respective tower, communicates only with the inner chamber for housing the heat source, whereas at the outer it communicates with an end of a respective duct 73 and 74, whose other end communicates with a respective inlet/outlet 75, 76 of valve means comprising a pressurizing valve 77 placed on the delivery side 8 of the hopper 1. The pressurizing valve 77 functions in order to assure a minimum pressure at the low flow-rates and avoid in the mean time an excessive pressure loss at the high flow-rates during the regeneration step of one of the towers 68, 69.

As illustrated in more detail in FIG. 5, the pressurizing valve 77 delimits an inner chamber in direct communication with the inlets/outlets, whereas it can communicate with an outlet at the top 79 through an opening 80 provided in a partition 81 and interceptable by a shutter means 82. The output 79 is, in turn, in communication with duct 8 for feeding dry air to the hopper 1.

The shutter 82 is supported by a rod or pin 83 slidingly mounted in a substantially vertical direction within the chamber 78 in any suitable way. Preferably, the shutter 82 is mounted at the top of pin 83 through a securing screw 84 screwing at the head of pin 83, and the pin-shutter-securing screw assembly forms a whole integral in movement and having a predetermined weight. With this construction of the pressurizing valve, the pressure of the air within the chamber 78 at the opening 80 exerts a force in contrast with the weight of the pin-shutter-screw assembly. When the air pressure is such that the shutter is caused to lift, e.g. 7-10 mbars, air can also flow through the opening 80 to the outlet 79 and duct 8.

If desired, the shutter means 80, instead of acting by gravity, can be elastically loaded in any suitable way, e.g. by means of one or more gauged springs, not shown in drawings.

The operation of the above described plant will be explain below with reference to the presence of two dehumidifying towers, as illustrated in FIG. 1, understanding that the number of dehumidifying towers can be varied from one to more than two.

In the diagram illustrated in FIG. 1, hot and dry air is supplied to the hopper 1 from the dehumidifying tower 69, whereas the regeneration tower 68 is subject to a regeneration cycle of the molecular sieves 67. The electrical resistor 70 heats the air supplied by duct 73, and a heat probe, through an electronic control unit 15, is arranged to control current supply to the electrical resistor 70, while maintaining the temperature of the air heated within the tower at about 300° C., before passing through the molecular sieves 67. The heated air passes through the molecular sieves 67 from the bottom to the to, regenerating them and then discharges into the duct 65 carrying out therewith the humidity taken away from the molecular sieves. Within duct 65 there is also provided a heat probe 86, which detects the temperature of the air coming out from the regeneration tower 68, and, when this reaches a predetermined value, sends a control signal to the electronic control unit 15 thereby cutting off the current supply to the resistor 70 for heating air. At this point, a cooling step of the tower 68 begins.

The duct 65 supplies air loaded with humidity coming from the tower 68 to the inlet 31 of the slide valve assembly 24, which, in the illustrated working trim, i.e. with the shutter 56 closing the opening 50, and the shutter 57 closing the opening 51 a, provide to deviate, through the side chamber 45, the air flow to the duct 35, and thus to supply the same to the inlet 38 of the diaphragm valve 39. The air enters into the compartment 40 through the inlet 38, and discharges outward through openings 43. The compartment 40, due to the action of the pressure diaphragm opposite controlled in the compartment 41, is continuously gauged, thereby assuring a controlled amount of regeneration humid air to pass. Until the compartment 41 is in a depressurised condition, the inlet 38 communicates with the openings 43, and such a condition is held during both the heating step of the regeneration air and the subsequent cooling operation of the dehumidification that is being regenerated.

When the regeneration of the tower 68 is ended, if the other tower 69 that is dehumidifying the process air is not yet saturated with humidity, the diaphragm valve 39 is closed, i.e. the solenoid valve 27 is driven by the control unit 25 thereby switching so to feed pressurized air to the compartment 38, closing it (FIG. 2), thereby “insulating” the regenerate tower 68 from the remaining plant.

Clearly, whereas the tower 68 is regenerated or results insulated, the other tower 67 continuously carries out the dehumidification of the process air to be fed to the hopper 1. More precisely, the process air enters in the intermediate chamber 47 of the valve group 24 from the delivery duct 23, passes through the opening 51, now free, and lets in the duct 66 to enter into the peripheral annular chamber housing the molecular sieves 67 of the tower 69. Once the process air has been entered into the tower 69, it passes through the molecular sieves from the top to the bottom of the tower itself, while transferring thereto the humidity that it carries. The air temperature is checked by the heat probe 85 at the bottom of the tower, and the process air rises again dehumidified along to the tower inner chamber, where it is heated by the resistor 70 contained therein, and exits dry and hot at the top through the outlet 72 and the duct 74, and reaches the inlet 76 of the pressurizing valve 77.

The pressurizing valve 77 has the particular task to assure a minimum pressure, e.g. 7-10 mbars, is held within the ducts 73 and 74, that is necessary to guarantee a constant supply of dry air during the regeneration process within the regeneration tower, the tower 68 in the case illustrated in FIG. 1.

The air passing through the outlet 79 of the pressurizing valve 77 by means of the duct 8 is supplied to the diffuser 11, thereby passing through the granular material bulk stored within the hopper 1, so then to exit and be sucked by the blower 13 through the duct 5, the filter 21, and the cooling battery 18.

When the tower 69 becomes saturated, the role of the towers has to be inverted, and to this end the control unit 15 will send a control signal to the motor 53 so to cause the slide valve assembly 24 changes its trim in order to move the shutter to open the opening 50 and close the opening 50 a, whereas the shutter 57 will open the opening 51 a and close the opening 51, in the mean time compressing the spring 61 until the microswitch will collide against the fixed contact 64. As a result of the new trim of the valve assembly 24, the regenerated tower 68 will be put in communication with the delivery side of the blower 13 through the chamber 47 and the opening 50, and it will supply dry and hot process air to the tower 1 through the pressurizing valve 77.

When designing a traditional dehumidification plant, normally one did consider the flow rate of dehumidified material necessary to supply one or more transformer machines, typically injection presses and/or extruders, with the same running at the maximum production. According to such a flow rate of material to be processed, typically expressed in Kg/h, and the time necessary to dehumidify the same, one did determine the granular material storage and feeding capacity of a hopper. Also the flow rate of dry and hot air fed by the hopper was traditionally determined as a function of the maximum flow rate of granular material feedable to a processing machine, as well as by considering the material most difficult to be dehumidified, e.g. a highly hygroscopic material. As a result, there was a clear trend to oversize the traditional dehumidification plants.

Dies of injection presses can normally be supplied by a granular material amount lower than that corresponding to the maximum flow rate (in terms of quantity of injectable material) of the processing machine. So, for example, for moulded pieces having a thin wall and/or a wide surface, it occurs to employ a great press, a great closing force of the dies being necessary. Nevertheless, only a few percentage of the maximum material flow rate is used, which would be injected into the press. The traditional injection presses available on the market are thus suitable to be adapted to the real moulding requirements with consequent save of energy.

On the contrary, the traditional dehumidification plants for granular material designed to supply the injection presses are rigid, in other words the are not capable to adapt themselves to any changes of the granular material supply to a downwards processing machine. For this reason, they feed always the same amount of granular material and dry and hot air in the time unit, which quantities are set during the plant calibration step, which leads to a high employ of energy, thereby generating a heat stress within the granular material, caused by the high stay time of the same at high temperature, caused by the drawing being decreased and a very high flow of hot air being held.

The dehumidification plant according to the present invention, differently from the traditional plants, is a flexible system, i.e. it is capable to appropriately control and adjust according to the variation of the operation conditions of the downwards processing machine(s) a great number of variables, i.e. in particular: specific air flow rate, air flow rate, production in the time unit, and the stay time of the material within the hopper 1.

In the present document, specific air flow rate refers to the amount of hot and dry air which has to be supplied per each of material to be dehumidified. So, for example, a specific air flow rate of 2 is the same as to supply 2 of air per each of a given granular material to be dehumidified, e.g. ABS (acyinitrile-butadiene-styrene).

The production in the time unit refers to the required per-hour flow rate expressed in of granular plastic material to be dehumidified. To determine such a variable, it occurs to consider the per-hour consumption of granular material by the injection press. In order to calculate the required air flow rate, one has always to multiply the above defined production of the specific air flow rate for that given material to be dehumidified. So, for example, if for a given processing machine the per-hour consumption of granular material is of 30 kg/h, to which it correspond a specific air flow rate of 2 m³/kg, it will be necessary a per-hour flow rate of dry and hot air of 30 kg/h×2 m³/kg=60 m³/h.

A dehumidification plant according to the present invention is thus provided with means suitable for varying the rate of the blower 13 driven by the electronic control unit 15, which permits the air flow rate outing from the blower 13 to be varied. Such a means suitable for varying the rate of the blower is preferably of a mechanical-type, and more preferably of electronic-type, e.g. an inverter 87 of any suitable type arranged to vary frequency of the current supplied to the motor 14 of the blower 13. Owen to the presence of the inverter 87, the dehumidification plant can operate in a flexible way, thereby adapting itself to requirements of a minimum amount of granular material per time unit, which permit a substantial saving of heat energy to be obtained.

To this end, in a first portion of memory of the control unit 15 a table is stored, which includes a list of a first multiplicity of granular plastic materials, together with respective main processing parameters, to be used in the plant. At a second portion of the control unit memory will be further possible to store processing parameters and characteristics relating to further experimentally obtained materials (experimental materials).

Once a specific granular material to be dehumidified among those listed in the table or an experimental material, as well as the per-hour consumption of dried granular material to be fed through the hopper 1 to be supplied to one or more processing machines (consumption) placed downwards to the dehumidification plant has been selected, the control unit 15 will

The invention as described above is susceptible to numerous modifications and variations within the scope as defined by the claims. 

1. A dehumidification plant for granular materials including at least one silo or hopper (1) for containing and dehumidifying granular material (2), which is provided with a controlled lower supplying mouth (3) arranged to receive at its top granular material (2) to be dehumidified, at least one feeding duct (8, 10) for hot and dry process air designed to draw within the granular material (2) contained in each hopper (1), and at least one exhaust duct (5) for humid process air; at least two molecular sieve towers (68, 69) arranged to alternately supply hot and dry process air to each hopper, each delimiting a housing chamber for molecular sieves and a housing chamber for heating means, said housing chambers being in communication one with another at an end thereof, whereas they are in communication, at their other end, with a respective air inlet/outlet duct; pressurizing or pumping means arranged to receive, at the suction (inlet) side, humid process air from said at least one exhaust duct, and to feed at the delivery side, pressured air to each molecular sieve tower; switching-shunting means placed between the delivery side of said pressurizing means and said inlet/outlet ducts of said housing chambers for molecular sieves in order to switch at least one of said molecular sieve towers between a process step and a regeneration step; and a programmable electronic control unit, characterized in that it comprises pressurizing valve means placed between said inlet/outlet ducts of said housing chamber of said heating means for each molecular sieve tower and arranged to assure a minimum pressure within a tower during the regeneration step, and detecting means for temperature electrically connected to said programmable electronic control unit, at its input.
 2. A plant as claimed in claim 1, characterized in that said valve means (77) comprises an inner chamber (78) in direct communication with said inlet/outlet ducts (73, 74), and in communication with an outlet (79) to at least one feeding duct (8) through an opening (80), which can be intercept by a shutter means (82) provided with a gauged opening/closing in function of the pressure within said inner chamber (78).
 3. A plant as claimed in claim 2, characterized in that said shutter means (82) is supported by a rod or pin (83) slidingly mounted in a substantially vertical direction within the inner chamber (78), thereby opening and closing for gravity owing to the pressure variation of the air in said chamber (78).
 4. A plant as claimed in claim 3, characterized in that said shutter means is elastically loaded in a gauged way, thereby opening and closing proportionally to the pressure within said inner chamber (78).
 5. A plant as claimed in any previous claim, characterized in that it comprises intercepting means (39) in communication with at least one exhaust (38) from said switching-shunting means (24) and drivable by a means (27) designed to detect the pressure differential between the suction side (25) and the delivery side (29) of said pressurizing means (13).
 6. A plant as claimed in claim 5, characterized in that said intercepting means comprises a diaphragm valve (39), whose diaphragm (42) delimits two inner compartments (40, 41), a compartment (40) communicating with at least one exhaust opening (43), whereas the other (41) is in fluid communication with said pressure differential detecting means (27).
 7. A plant as claimed in claim 5 or 6, characterized in that said pressure differential detecting means comprises a solenoid valve (27) having two inlets (26, 28) in fluid communication with, respectively, the suction side and the delivery side of said air pressurizing means (13), and its outlet (44) in fluid communication with said compartment (41).
 8. A plant as claimed in any previous claim 5 to 7, characterized in that said switching-shunting means comprises a slide valve means (24), and driving means (52-55) of said slide valve assembly designed to drive it both in a continuous and pulsating way.
 9. A plant as claimed in claim 6, characterized in that said slide valve assembly (24) presents a valve body internally delimiting two side chambers (45, 46), and a intermediate chamber (47), which communicate each other through openings (50, 51), said intermediate chamber communicating with the delivery side of said air pressurizing or pumping means (13), whereas said side chambers (45, 46) communicate with both a respective air inlet/outlet duct (65, 66) and a respective exhaust opening (50 a, 51 a) to said intercepting means (39), and comprises a rigid rod (52), which extends through said side chambers (45, 46) and intermediate (47), supports a pair of shutter means (56, 57) fixed thereto and designed to open-close said openings (50, 51; 50 a, 51 a), and exits from the valve body thereby cinematically connecting to said driving means.
 10. A plant as claimed in claim 9, characterized in that said driving means comprises a reversible linear operating means including a reversible electric motor (53) drivable by a programmable electronic control unit (15) and a reducer (54), and a rack (55) cinematically connected to said reducer and moving integral with said rigid rod (52).
 11. A plant as claimed in claim 9, characterized in that said linear operating means comprises two spaced stops (58, 59) fixed on said rigid rod (52), an elastic loading means (60, 61) for each stop designed to abut against a member fixed with respect to said rigid rod (52), a pair of micro-switches (62, 63) carried by the rod (52) and arranged to abut against a intermediate contact (64) fixed with respect to the rod (52) and arranged to permit said reversible motor (53) to stop at two working positions of said shutters (56, 57).
 12. A plant as claimed in any previous claim, characterized in that it comprises cooling means designed to cool the air flowing in said at least one exhaust duct (5) for humid process air directed to said air pressurizing means (13).
 13. A plant as claimed in claim 12, characterized in that said cooling means comprises an assembly of parallel pipes (18) subjected to the action of at least one fan (19) operable by a respective electric motor (20).
 14. A plant as claimed in any previous claim, characterized in that it comprises a heat probe (86) arranged to detect the temperature of the air coming out the regeneration tower (65), and electrically connected to said programmable electronic control unit (15).
 15. A plant as claimed in any previous claim, characterized in that said programmable electronic control unit (15) includes a first memory portion designed to store treating parameters concerning a first multiplicity of granular materials, and a second memory portion designed to store treating parameters of experimental materials.
 16. A plant as claimed in any previous claim, characterized in that it comprises a user interface (91) with said programmable electronic control unit (15).
 17. A plant as claimed in claim 16, characterized in that said user interface (91) comprises a display unit, and data inputting means in said programmable electronic control unit (15).
 18. A plant as claimed in claim 17, characterized in that said display unit is of touch-screen type.
 19. A plant as claimed in any previous claim, characterized in that it comprises adjusting means (87) controlled by said programmable electronic control unit (15) and designed to adjust the air flow-rate coming out from said pressurizing and pumping means (13).
 20. A plant as claimed in claim 19, characterized in that said adjusting means (87) of the air flow-rate coming out from said pressurizing and pumping means (13) comprises an inverter (87).
 21. A plant as claimed in any previous claim, characterized in that it comprises means (92) form measuring the air flow-rate entering into the hopper 1 electrically connected with said programmable electronic control unit (15).
 22. A plant as claimed in claim 21, characterized in that said flow-rate measuring means comprises a Venturi tube (92).
 23. A method for regenerating a molecular sieve tower (68) in a dehumidifying plant for granular material as claimed in any claim 1 to 22, comprising, in sequence, heating of the molecular sieved (67) to a temperature of about 300° C., and cooling the molecular sieves, characterized in that said cooling comprises the controlled mixing of the air within the tower to be cooled (68) by means of process air coming from another molecular sieve tower (69), said mixing being controlled through said switching-shunting means (24) in response to the temperature detected by said temperature detecting means (9).
 24. A method as claimed in claim 23, characterized in that said mixing through said switching-shunting means (24) is carried out in a gradual or pulsating way.
 25. A method as claimed in claim 24, characterized in that said tower (68) to be cooling during the mixing step is isolated from the outer by intercepting means (39).
 26. A method as claimed in any claim 23 to 25, characterized in that it comprises a waiting step for said tower to be cooled when its cooling is ended.
 27. A method as claimed in any claim 23 to 26, characterized in that it comprises a hot and dry air flow-rate modulating step within said air pressurizing or pumping means (13), which is controlled by said programmable electronic control unit (15). 